Dual function filtration and catalytic breakdown of organic pollutants in wastewater using ozonation with titania and alumina membranes

被引:47
|
作者
Zhu, Bo [1 ]
Hu, Yaoxin [1 ,2 ]
Kennedy, Stephen [1 ]
Milne, Nicholas [1 ]
Morris, Gayle [3 ]
Jin, Wanqin [2 ]
Gray, Stephen [1 ]
Duke, Mikel [1 ]
机构
[1] Victoria Univ, Inst Sustainabil & Innovat, Melbourne, Vic 8001, Australia
[2] Nanjing Univ Technol, State Key Lab Mat Oriented Chem Engn, Nanjing 210009, Jiangsu, Peoples R China
[3] Flinders Univ S Australia, Res Serv Off, Adelaide, SA 5001, Australia
基金
澳大利亚研究理事会;
关键词
Water reuse; Filtration; Ozonation; Ceramic membrane; Titania; TIO2/AL2O3 COMPOSITE MEMBRANES; CROSS-FLOW MICROFILTRATION; PHOTOCATALYTIC TIO2 FILMS; SOL-GEL PREPARATION; CERAMIC MEMBRANES; NANOFILTRATION MEMBRANES; HUMIC SUBSTANCES; REVERSE-OSMOSIS; SURFACE-AREA; PERFORMANCE;
D O I
10.1016/j.memsci.2010.11.045
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Water recycling via treatment from industrial and/or municipal waste sources is one of the key strategies for resolving water shortages worldwide. Polymer membranes are effective at improving the water quality essential for recycling, but depend on regular cleaning and replacement. Pure ceramic membranes can reduce the cleaning need and last significantly longer in the same applications while possessing the possibility of operating in more aggressive environments not suitable for polymers. In the current work, filtration using a tubular ceramic membrane (alpha-Al(2)O(3) or TiO(2)) was combined with ozonation to remove organic compounds present in a secondary effluent to enhance key quality features of the water (colour and total organic carbon, TOC) for its potential reuse. 'Bare' commercial alpha-Al(2)O(3) filters (pore size similar to 0.58 mu m) were tested as a microfiltration membrane and compared with the more advanced catalytically active TiO(2) layer that was formed by the sol-gel method. The presence of anatase with a 4 nm pore size at the membrane surface was confirmed by X-ray diffraction (XRD) and N(2) adsorption. Filtration of the effluent over a 2 h period led to a reduction in flux to 45% and 60% of the initial values for the a-alumina and TiO(2) membrane, respectively. However, a brief dose (2 min) of ozone at the start of the run resulted in reductions to only 70% of the initial flux for both membranes. It is likely that the oxide's functional property facilitated the formation of hydroxyl (OH center dot) or other radicals on the membrane surface from ozone decomposition which targeted the breakdown of organic foulants thus inhibiting their deposition. Interestingly, the porous structure therefore acted in a synergistic, dual function mode to physically separate the particulates while also catalytically breaking down organic matter. The system also greatly improved the efficiency of membrane filtration for the reduction of colour, A(254) (organics absorption at the wavelength of 254 nm) and TOC. The best performance came from combined ozonation (2 min ozonation time with an estimated applied ozone dose of 8 mg L(-1)) with the TiO2 membrane, which was able to reduce colour by 88%, A(254) by 75% and TOC by 43%. It is clearly evident that a synergistic effect occurs with the process combination of ozonation and ceramic membrane filtration demonstrating the practical benefit of combining ceramic membrane filtration with conventional water ozonation. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:61 / 72
页数:12
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